IE863060L - Preparing 5-(2,5-dimethylphenoxy)-2,2-dimethyl-pentanoic¹acid. - Google Patents
Preparing 5-(2,5-dimethylphenoxy)-2,2-dimethyl-pentanoic¹acid.Info
- Publication number
- IE863060L IE863060L IE863060A IE306086A IE863060L IE 863060 L IE863060 L IE 863060L IE 863060 A IE863060 A IE 863060A IE 306086 A IE306086 A IE 306086A IE 863060 L IE863060 L IE 863060L
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- IE
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- Prior art keywords
- dimethylphenoxy
- toluene
- dimethylsulfoxide
- alkali metal
- lower alkyl
- Prior art date
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/02—Esters of acyclic saturated monocarboxylic acids having the carboxyl group bound to an acyclic carbon atom or to hydrogen
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/347—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/347—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
- C07C51/367—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by introduction of functional groups containing oxygen only in singly bound form
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- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Luminescent Compositions (AREA)
Abstract
An improved two-step process for preparing 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid (gemfibrozil) which regularly affords gembibrozil in overall yields in excess of 80% comprises reacting an alkali metal salt of a lower alkyl ester of 2-methylpropanoic acid with 1,3-dibromopropane or 1-bromo-3-chloropropane in a polar aprotic solvent such as tetrahydrofuran, and then reacting the intermediate thus formed with an alkali metal salt of 2,5-dimethylphenol in a mixed toluene/dimethylsulfoxide solvent system.
Description
59499 The present invention relates to chemical processes for preparing (substituted-phenoxy)alkanoic acids and esters. More particularly, the present invention concerns an improved process for preparing 5 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid.
Substituted phenoxyalkanoic acids as a class have been found to regulate blood lipid levels and to possess utility as agents for the treatment or prevention of arteriosclerosis. (See, for example, 10 United States Patents 3,674,836 to Creger, 4,238,492 to Majoie, and 4,351,950 to Sircar.) In particular, the compound 5-(2,5-dimethyl-phenoxy)-2,2-dimethylpentanoic acid, known generically as gemfibrozil, has been shown to be effective in 15 elevating blood serum levels of high-density lipoproteins while simultaneously lowering the levels of low-density serum lipoproteins. (See, for example, P. Samuel, "Effects of Gemfibrozil on Serum Lipids," Am. J. Med.. May 23, 1983, pp. 23-27. 20 United States Patent 3,674,836, discloses gemfibrozil and several analogues together with a process for their preparation.
United States Patent 4,351,950 discloses phenylene-bis-alkoxyalkanoic acids and esters and two 25 processes for their production. 9- i -3- . In accordance with the present invention, a process for preparing 5-(2,5-dimethylphenoxy)-2,2-J dimethylpentanoic acid (gemfibrozil) comprises the steps of: a) reacting a lower alkyl ester of 5 .2-methylpropanoic acid with an alkali metal salt of a di-(lower alkyl)amine in a polar aprotic organic solvent to produce an alkali metal salt of formula I (CH.,) --C-COOR J (-) M ( + ) wherein R is lower alkyl and M is an alkali metal, and 10 then with a 1,3-dihalopropane selected from 1-bromo-3-chloropropane and 1,3-dibromopropane at a temperature above about -20°C to produce an intermediate of the formula X-CH2CH2CH2C(CH3)2COOR wherein X is chlorine or bromine and R is as defined above; b) reacting said intermediate with an alkali metal salt of 2,5-dimethylphenol to produce 5-(2,5-dimethyphenoxy-2,2-dimethylpentanoic acid in yields greater than 80% from said lower alkyl ester of 2-methylpropanoic acid. 15 20 United States Patent 3,674,836 teaches the preparation of 5-(2,5-dimethylphenoxy)-2,2-dimethyl-pentanoic acid (gemfibrozil) by a two step process in ) which 2,5-dimethylphenol is first O-alkylated with 25 1,3-dibromopropane to yield 1-(2,5-dimethylphenoxy)-3-bromopropane in accordance with the procedure -4- described by Marvel et al., Org. Synth., Collective Vol. I, pp 435-436, John Wiley & Sons, New York, 1941. Typical yields reported there for this reaction vary between 55-60%. 5 In the second step, the 1-(2,5-dimethylphenoxy)-3- bromopropane is reacted with the dianion of isobutyric acid, i.e.
CH, I 3 - + CH^-C-COO M M+ where M is an alkali metal ion, to give 5—(2,5— 10 dimethylphenoxy)-2,2-dimethylpentanoic acid (gemfibrozil) in accordance with the procedure described by Creger in Org. Synth., Vol. 50, pp. 58-62, John Wiley & Sons, New York, 1970. Typical yields reported there for this reaction vary between 70-76%. 15 Thus, for this prior art process, typical overall yields range from a low of about 39% to a high of about 46%. | In contrast, the process of the present invention produces gemfibrozil from readily available starting 20 materials in overall yields which regularly exceed 70%, frequently exceeding 80%. The process comprises first preparing a lower alkyl ester of 5-bromo- or 5-chloro- 2.2-dimethylpentanoic acid which ester is then used to O-alkylate an alkali metal salt of 2,5-dimethylphenol. 25 In the first step of the present process, a lower alkyl ester of 2-methylpropanoic acid (isobutyric acid) is C-alkylated with either l-bromo-3-chloropropane or 1.3-dibromopropane to yield the corresponding lower alkyl ester of 5-bromo- or 5-chloro-2,2-dimethyl- 30 pentanoic acid. This step of the process involves the initial formation of an alkali metal salt of the carbanion at the tertiary carbon atom of the isobutyric acid ester followed by its alkylation with the , 1,3-dihalopropane and is carried out in a single reaction vessel.
The term "lower alkyl ester" is intended to 5 encompass alkyl ester groups of from one to four carbon atoms, including methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, iso-butyl, and tert-butyl.
Higher yields are obtained from this alkylation step when the starting materials are the preferred 10 ester, 2-methylpropyl 2-methylpropanoate (isobutyl isobutyrate) and the preferred dihalide l-bromo-3-chloropropane.
This alkylation step of the process is carried out in an anhydrous polar aprotic organic solvent such as 15 tetrahydrofuran, tetrahydropyran, dimethoxyethane, diethylene glycol dimethyl ether, and the like. The preferred solvent is tetrahydrofuran.
An alkali metal such as lithium or sodium is combined with the aprotic solvent, and a di-(lower 20 alkyl)amine, followed by a conjugated olefin such as styrene, methyl styrene, isoprene, or naphthalene, to produce the corresponding alkali metal di(lower alkyl)amide. The preferred materials are lithium and diisopropylamine. The formation of the alkali metal 25 di-(lower alkyl)amide is carried out at temperatures ranging from about 20°C to about 60°C, with preferred temperatures lying in the range from about 30°C to about 5 0 ° C.
The lower alkyl ester of 2-methylpropanoic acid is 30 next added while maintaining the temperature of the i reaction mixture between about -20°C to about 20°C, preferably between about 5°C to about 15°C. To this J mixture is next added the l-bromo-3-halo-propane, while still maintaining the temperature of the reaction -6- mixture between about 0°C and 20°C, preferably between about 5°C and 15°C. The mixture is stirred for a period of from about 2 to about 15 hours, preferably about 12 hours after which the reaction is quenched by 5 the addition of water, and the mixture is partitioned between water and a non-polar hydrocarbon solvent such as hexane. The organic phase is separated, optionally dried over an anhydrous dessicant such as magnesium sulfate, and the solvent removed. The residual lower 10 alkyl ester of 5-bromo- or 5-chloro-2,2-dimethylpentanoic acid is purified by distillation; Although either 1,3-dibromopropane or l-bromo-3-chloropropane may be employed as the alkylating reagent in this step of the process, l-bromo-3-chloropropane is 15 preferred because of the higher yields that result. A comparison of the yields in employing the two materials is apparent from Examples 3 and 4. In Example 3, the preferred l-bromo-3-chloropropane reagent was employed and the yield of methyl 5-chloro-2,2-dimethylpentanoate 20 ester intermediate on a commercial scale was 81%. However, when the alternative 1,3-dibromopropane starting material was employed, as in Example 4, the yield of methyl 5-bromo-2,2-dimethylpentanoate on a comparable scale was only 67%. Formation of the 25 undesired by-product formed from reaction of both bromine atoms of the 1,3-dibromopropane with two equivalents of the methyl lithioisobutyrate, which might otherwise be expected to diminish the yield of desired product, was minimized by "reverse addition" of 30 the solution of the lithium salt to excess dibromide. In spite of this precaution, the yield of desired product was still lower than when the preferred l-bromo-3-chloropropane starting material is employed. -7- As illustrated by Examples 2 and 3, the yield of the 5-chloro-2,2-dimethylpentanoate ester intermediate is greater when the preferred 2-methylpropyl 2-methylpropanoate (isobutyl isobutyrate) starting 5 ester is employed. Thus, in Example 2, the yield of 2-methylpropyl 5-chloro-2,2-dimethylpentanoate was 94%, while use of the alternative starting ester, methyl 2-methylpropanoate (methyl isobutyrate) in Example 3 yielded only 81% of the desired intermediate. 10 In the second step of the process of this invention, 2,5-dimethylphenol is dissolved in a mixture of a higher-boiling non-polar hydrocarbon solvent and a polar solvent. The solution is then reacted with a strong base to produce the corresponding 15 2,5-dimethylphenolate salt. An alkali metal hydroxide such as sodium hydroxide or potassium hydroxide is preferred, and the mixture is heated under reflux with provision for the azeotropic removal of water from the reaction mixture as the 2,5-dimethylphenol is converted 20 to the corresponding alkali metal phenolate. Although either sodium or potassium hydroxide may be employed, the preferred alkali metal hydroxide is sodium hydroxide because of its lower cost.
The alkali metal phenolate is then reacted with 25 the 5-bromo- or 5-chloro-2,2-dimethylpentanoate ester to produce gemfibrozil. The reaction is generally carried out under reflux in the mixed solvent system for a period of from about 7 to about 20 hours.
Suitable higher-boiling non-polar solvents include 30 benzene, toluene and the xylenes, with tolune being preferred. Suitable polar solvents include dimethyl sulfoxide, dimethylformamide, dimethyl ether of ethylene glycol and similar ethers, with dimethyl sulfoxide being preferred. -8- The preferred mixed solvent system for this step of the reaction comprises from about 5 to about 15 parts (volume/volume) of toluene to one part dimethylsulfoxide. It has been found that in solvent 5 systems employing ratios of toluene to dimethylsulf-oxide greater than about 15:1 or less than 5:1, the yield of desired product falls off. More preferred ratios of toluene to dimethylsulfoxide lie in the range of about 5:1 to about 10:1, with optimum results being 10 obtained with a ratio of toluene to dimethylsulfoxide at about 7.5:1.
As shown by Examples 5 and 6, a higher yield in this second step of the reaction is also obtained when the preferred intermediate 2-methylpropyl 5-chloro-2,2-15 dimethylpentanoate is employed. In Example 5, when this preferred intermediate was used, the yield of gemfibrozil was 92%, while the yield in Example 6 for this step was lowered to 86% when the corresponding methyl ester was employed. 20 Thus for the two step process of the present invention, overall yields of greater than 80% are realized as compared with considerably lower yields for the prior art process.
The following examples are provided to enable one 25 skilled in the art to practice the invention. These examples are merely illustrative of the process of this invention and should not be read as limiting the scope of the invention as it is defined by the appended claims.
I -9- Example 1 Preparation of Methyl 5-Chloro-2,2-dimethylpentanoate Lithium metal shot (6.31 g, 0.91 mol) was weighed under an argon atmosphere and placed in an 5 argon-filled 1-liter flask. Tetrahydrofuran (182 ml) and diisopropylamine (96.6 g, 0.955 mol) were added. The mixture was heated to 35°C while styrene (48.8 g, 0.468 mol) was added slowly while maintaining the temperature between 35°C and 42°C. 10 When the addition of styrene was complete, and the exotherm had subsided, the mixture was cooled and methyl isobutyrate (83.6 g, 0.819 mol) was added dropwise at 5°C to 10°C.
Next, l-bromo-3-chloropropane (193.7 g, 1.23 mol) 15 was added at temperatures between 10°C and 35°C (mainly below 15°C) and the mixture was allowed to warm to room temperature over a period of three days. The reaction mixture was then quenched by the addition of 40 ml of water, and the volume of the solution was reduced to 20 200 ml under vacuum. This residue was partitioned between 200 ml of hexane and 200 ml of water. The layers separated, and the aqueous layer was washed weith 100 ml of hexane. The combined organic layers were distilled and the product .fraction collected at 25 56°C to 62°C (4 torr, 0.52 kPascal) to yield 107.7 g (74%) of methyl 5-chloro-2,2-dimethylpentanoate.
Example 2 Preparation of 2-Methylpropyl 5-Chloro-2.2-dimethylpentanoate (Commercial Scale) 30 Employing, generally, the method of Example 1, 1.6 kg (0.230 kg-mol) of lithium metal was treated with -10- 40.8 kg of dry tetrahydrofuran and 25.7 kg (0.254 kg-mol) of diisopropylamine followed by reaction with 12.68 kg (0.121 kg-mol) of styrene at temperatures between about 35-40°C. 5 After reaction with the lithium metal was essentially complete, the mixture was cooled to temperatures between 5-15°C and 30 kg (0.208 kg-mol). of 2-methylpropyl 2-methylpropanoate (isobutyl isobutyrate) was slowly added. 10 The reaction mixture was again cooled to temperatures between about 5-15°C and 42.5 kg (0.270 kg-mol) of l-bromo-3-chloropropane was slowly added. After addition was complete, the mixture was allowed to warm to 14°C over a period of about 13 hours. 15 The final reaction mixture was quenched with 11.5 liters of water, the tetrahydrofuran removed, and the residue diluted with 75 liters of water and extracted with hexane. Removal of the hexane and distillation of the residue yielded 43 kg (0.195 kg-mol, 94%) of 20 2-methylpropyl 5-chloro-2,2-dimethylpentanoate, bp 94-98°C at 4 Torr (0.53 kPascal).
Example 3 Preparation of Methyl 5-Chloro-2,2-dimethylpentanoate (Commercial Scale) 25 Employing, generally, the method of Example 2, 23.3 kg (0.218 kg-mol) of lithium diisopropylamide was prepared and reacted with 19.1 kg (0.187 kg-mol) of methyl 2-methylpropanoate (methyl isobutyrate) in ■* tetrahydrofuran at temperatures' between about 5-15°C. 30 Reaction of the intermediate thus formed with 38.5 ;kg (0.244 kg-mol) of l-bromo-3-chloropropane yielded, after work-up as described in Example 2, 27.1 kg (81%) of methyl 5-chloro-2,2-dimethylpentanoate, bp 72°C at 6 ;-11- ;torr (0.78 kPascal). ;Example 4 ;Preparation of Methyl 5-Bromo-2,2-dimethylpentanoate Employing, generally, the method of Example 3, a 5 tetrahydrofuran solution of 179.4 kg (1.66 kg-mol) of the lithium salt of methyl 2-methylpropanoate (methyl lithioisobutryrate) was added to 501 kg (2.48 kg-mol) of 1,3-dibromopropane, maintaining the temperature of the reaction mixture at temperatures between about 10 0-10°C. After the reaction was complete, the mixture was stirred for 48 hours. ;The reaction was then quenched by the addition of water, and the tetrahydrofuran was stripped from the mixture. The residue was partitioned between 600 15 liters of water and 80 kg of dichloromethane and acidified with hydrochloric acid. The water layer was extracted with 133 kg of dichloromethane and the combined organic layers were distilled to yield 248 kg (67%) of methyl 5-bromo-2,2-dimethylpentanoate, bp 20 60-65°C at 1 torr (0.13 kPascal). ;Example 5 ;Preparation of 5-(2,5-Dimethylphenoxy-2,2-dimethylpentanoic Acid (Starting with 2-Methylpropyl 5-Chloro-2,2-dimethylpentanoate) ;25 To a solution of 21.99 kg (0.180 kg-mol) of ;2,5-dimethylphenol in 135 liters of toluene and 18 liters of dimethylsulfoxide were added 7.8 kg (0.195 kg-mol) of sodium hydroxide. The mixture was heated under reflux until all of the water had been 30 azeotropically removed, and 2.83 kg (0.019 kg-mol) of sodium iodide were added. ;2-Methylpropyl 5-chloro-2,2-dimethylpentanoate ;-12- ;(41.73 kg, 0.189 kg-mol) were added. The mixture was heated under reflux for an additional 13 hours, after which time 14.4 kg of sodium hydroxide were added and heating was continued for 4 hours. ;5 The toluene was removed by distillation, the crude product was partitioned between 90 liters of water and 30 liters of hexane, and the aqueous layer was acidified with hydrochloric acid to yield crude 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid 10 (gemfibrozil). Recrystallization from aqueous methanol solution yielded 41.5 kg (92%). ;Example 6 ;Preparation of 5-(2,5-Dimethylphenoxy)-2,2-dimethylpentanoic Acid (Alternative Method Starting with Methyl 15 5-Chloro-2,2-dimethylpentanoate) ;Employing, generally, the method of Example 5, 12.22 kg (0.100 kg-mol) of 2,5-dimethylphenol were reacted with 18.76 kg (0.091 kg-mol) of methyl 5-chloro-2,2-dimethylpentanoate. The yield of 20 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid (gemfibrozil) was 21.6 kg (86%). ;V *
Claims (1)
1. A process for preparing 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid comprising the steps of: a) reacting a lower alkyl ester of 2-methylpropanoic acid with an alkali metal salt of a di-(lower alkyl)amine in a polar aprotic organic solvent to produce an alkali metal salt of formula I (CH.,) --C-COOR Z(-) M ( + ) wherein R is lower alkyl and M is an alkali metal, and then with a 1,3-dihalopropane selected from l-bromo-3-chloropropane and 1,3-dibromopropane at a temperature above about -20°C to produce an intermediate of the formula X-CH2CH2CH2C(CH3)2COOR wherein X is chlorine or bromine and R is as defined above; b) reacting said intermediate with an alkali metal salt of 2,5-dimethylphenol to produce a iower alkyl ester of 5-(2,5-dimethyl-phenoxy)-2,-2-dimethylpentanoic acid and thereafter hydrolyzing said lower alkyl ester to produce 5-(2,5-dimethyl-phenoxy)-2,2-dimethylpentanoic acid. -14- Th e process in accordance with Claim 1 wherein said lower alkyl ester of 2-methylpropanoic acid is 2-methylpropyl 2-methylpropanoate. The process in accordance with Claim 1 wherein said 1-3-dihalopropane is l-bromo-3-chloropropane. The process in accordance with Claim 1 wherein step c) is carried out at reflux temperatures in a mixed solvent system of a non-polar hydrocarbon solvent and a polar solvent. The process in accordance with Claim 4 wherein said mixed solvent system comprises from 5 parts (V/V) toluene to 1 part (V/V) dimethylsulfoxide to about 10 parts (V/V) toluene to 1 part (V/V) dimethylsulfoxide. The process in accordance with Claim 4 wherein said mixed solvent system comprises about 7.5 parts (V/V) toluene to 1 part (V/V) dimethylsulfoxide. -15- A process for preparing 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid comprising the steps of: a) reacting 2-methylpropyl 2-methylpropanoate with lithium diisopropylamide and then with l-bromo-3-chloropropane at a temperature below about 25°C to produce 2-methylpropyl 5-chloro-2,2-dimethylpentanoate b) subsequently reacting said 2-methylpropyl 5-chloro-2,2-dimethylpentanoate with sodium 2,5-dimethylphenolate under reflux in a solvent comprising a mixture of from 10 parts (V/V) toluene/1 part (V/V) dimethylsulfoxide to 5 parts (V/V) toluene/1 part (V/V) dimethylsulfoxide, hydrolyzing the resulting ester, and thereafter acidifying the mixture and isolating 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid. The process of Claim 7 wherein said solvent comprises a mixture of about 7.5 parts (V/V) toluene to 1 part (V/V) dimethylsulfoxide. A process according to Claim 1 for preparing 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid, substantially as hereinbefore described with particular reference to the accompanying Examples. 5-(2,5-Dimethylphenoxy)-2,2-dimethylpentanoic acid whenever prepared by a process claimed in a preceding claim. F. R. KELLY & CO.f AGENTS FOR THE APPLICANTS.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US06/806,312 US4665226A (en) | 1985-12-09 | 1985-12-09 | Process for preparing 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid |
Publications (2)
Publication Number | Publication Date |
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IE863060L true IE863060L (en) | 1987-06-09 |
IE59499B1 IE59499B1 (en) | 1994-03-09 |
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Application Number | Title | Priority Date | Filing Date |
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IE306086A IE59499B1 (en) | 1985-12-09 | 1986-11-19 | Improved process for preparing 5-(2,5-dimethylphenoxy)-2,2-dimethylpentanoic acid |
Country Status (22)
Country | Link |
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US (1) | US4665226A (en) |
EP (1) | EP0226161B1 (en) |
JP (1) | JP2506094B2 (en) |
KR (2) | KR870005954A (en) |
CN (1) | CN1012896B (en) |
AT (1) | ATE47832T1 (en) |
AU (1) | AU590358B2 (en) |
CA (1) | CA1267155A (en) |
DE (1) | DE3666805D1 (en) |
DK (1) | DK174496B1 (en) |
ES (1) | ES2011245B3 (en) |
FI (1) | FI85974C (en) |
GR (1) | GR3000216T3 (en) |
HK (1) | HK112193A (en) |
HU (1) | HU195635B (en) |
IE (1) | IE59499B1 (en) |
IL (1) | IL80885A (en) |
IN (1) | IN166169B (en) |
NO (1) | NO164293C (en) |
PH (1) | PH24273A (en) |
PT (1) | PT83888B (en) |
ZA (1) | ZA868893B (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
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HU210180B (en) * | 1990-05-11 | 1995-02-28 | Egyt Gyogyszervegyeszeti Gyar | Process for preparing halogeneted polybasic esters |
US5235097A (en) * | 1990-05-11 | 1993-08-10 | Egis Gyogyszergyar | Process for the preparation of 2,2-dimethyl-5-(2,5-dimethyl-phenoxy)-pentanoic acid, intermediates for preparing this compound and process for preparing the intermediates |
US5041640A (en) * | 1990-09-20 | 1991-08-20 | Warner-Lambert Company | Process for mono-, di-, trisubstituted acetic acids |
BE1007058A3 (en) * | 1992-06-16 | 1995-03-07 | Omnichem Sa | A NEW METHOD FOR THE PREPARATION OF ACID 5- (2,5-dimethylphenoxy) -2,2-DIMETHYL pentanoic. |
IT1265087B1 (en) * | 1993-05-20 | 1996-10-30 | Recordati Chem Pharm | GEMFIBROZIL PREPARATION PROCESS |
US5530145A (en) * | 1994-06-14 | 1996-06-25 | Syn-Tech Chem & Pharm Co., Ltd. | Anticholesteremic compounds |
US5412112A (en) * | 1994-06-14 | 1995-05-02 | Industrial Technology Research Institute | Derivatives and preparation of 2,2-dimethyl-5-substituted phenoxy-pentanoic acids |
EP1627069A4 (en) * | 2002-08-08 | 2010-06-02 | Glaxosmithkline Llc | Methods for the isolation and purification of ansamitocins |
CN101440032B (en) * | 2008-11-13 | 2012-05-23 | 浙江大学 | Gemfibrozil polycrystalline type and preparation thereof |
WO2020212955A1 (en) * | 2019-04-18 | 2020-10-22 | Hikal Limited | Process for the preparation of a key intermediate of gemfibrozil |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
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US3674836A (en) * | 1968-05-21 | 1972-07-04 | Parke Davis & Co | 2,2-dimethyl-{11 -aryloxy-alkanoic acids and salts and esters thereof |
US3759986A (en) * | 1970-03-30 | 1973-09-18 | Parke Davis & Co | Esters of 2,2-dimethyl-5-(aryloxy)-1-pentanols |
US3707566A (en) * | 1970-03-30 | 1972-12-26 | Parke Davis & Co | Aryloxypentane compounds |
GB1422679A (en) * | 1972-11-16 | 1976-01-28 | Funai Pharmaceutical Ind Ltd | Substituted phenoxy-a-methylpropionic acid derivatives and a process for producing the same |
GB2025942A (en) * | 1978-05-31 | 1980-01-30 | Sori Soc Rech Ind | Phenoxyalkylcarboxylic acids |
ES8600261A1 (en) * | 1983-06-24 | 1985-10-01 | Yamanouchi Pharma Co Ltd | Phenoxy derivatives, their preparation, and pharmaceutical compositions containing them. |
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1985
- 1985-12-09 US US06/806,312 patent/US4665226A/en not_active Expired - Lifetime
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1986
- 1986-11-18 IN IN1005/DEL/86A patent/IN166169B/en unknown
- 1986-11-19 IE IE306086A patent/IE59499B1/en not_active IP Right Cessation
- 1986-11-24 AU AU65606/86A patent/AU590358B2/en not_active Ceased
- 1986-11-24 ZA ZA868893A patent/ZA868893B/en unknown
- 1986-11-25 CA CA000523753A patent/CA1267155A/en not_active Expired - Fee Related
- 1986-12-01 FI FI864900A patent/FI85974C/en not_active IP Right Cessation
- 1986-12-03 KR KR860010302A patent/KR870005954A/en not_active IP Right Cessation
- 1986-12-05 PH PH34561A patent/PH24273A/en unknown
- 1986-12-05 IL IL80885A patent/IL80885A/en unknown
- 1986-12-08 JP JP61290642A patent/JP2506094B2/en not_active Expired - Fee Related
- 1986-12-08 DE DE8686117076T patent/DE3666805D1/en not_active Expired
- 1986-12-08 ES ES86117076T patent/ES2011245B3/en not_active Expired - Lifetime
- 1986-12-08 EP EP86117076A patent/EP0226161B1/en not_active Expired
- 1986-12-08 NO NO864933A patent/NO164293C/en unknown
- 1986-12-08 HU HU865104A patent/HU195635B/en not_active IP Right Cessation
- 1986-12-08 AT AT86117076T patent/ATE47832T1/en not_active IP Right Cessation
- 1986-12-08 DK DK198605882A patent/DK174496B1/en not_active IP Right Cessation
- 1986-12-09 CN CN86108472A patent/CN1012896B/en not_active Expired
- 1986-12-09 PT PT83888A patent/PT83888B/en not_active IP Right Cessation
-
1987
- 1987-12-03 KR KR1019860010302Q patent/KR950003120B1/en active
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1989
- 1989-11-15 GR GR89400242T patent/GR3000216T3/en unknown
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1993
- 1993-10-21 HK HK1121/93A patent/HK112193A/en not_active IP Right Cessation
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